JPS586488Y2 - Coagulation device for dehydrator - Google Patents

Coagulation device for dehydrator

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Publication number
JPS586488Y2
JPS586488Y2 JP8900379U JP8900379U JPS586488Y2 JP S586488 Y2 JPS586488 Y2 JP S586488Y2 JP 8900379 U JP8900379 U JP 8900379U JP 8900379 U JP8900379 U JP 8900379U JP S586488 Y2 JPS586488 Y2 JP S586488Y2
Authority
JP
Japan
Prior art keywords
sludge
water
dehydrator
rotating body
hollow rotating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP8900379U
Other languages
Japanese (ja)
Other versions
JPS567514U (en
Inventor
忠昭 河杉
進 藤波
Original Assignee
株式会社クボタ
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 株式会社クボタ filed Critical 株式会社クボタ
Priority to JP8900379U priority Critical patent/JPS586488Y2/en
Publication of JPS567514U publication Critical patent/JPS567514U/ja
Application granted granted Critical
Publication of JPS586488Y2 publication Critical patent/JPS586488Y2/en
Expired legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【考案の詳細な説明】 本考案は、脱水機への供給前処理として水処理汚泥と凝
集剤とを混和するための凝集装置に関する。
[Detailed Description of the Invention] The present invention relates to a flocculation device for mixing water treatment sludge with a flocculant as a pretreatment for supply to a dehydrator.

上記装置において、従来、水処理汚泥を単に凝集処理し
ているにすぎず、特に低濃度汚泥に対して脱水処理負荷
が大で、脱水処理後のろ過物の含水率を低くシ、処理量
を多くする脱水性能の良い処理を行なわせられない欠点
があった。
Conventionally, in the above-mentioned equipment, water treatment sludge is simply flocculated, and the dewatering process is particularly heavy for low-concentration sludge. There was a drawback that it was not possible to perform a process with good dehydration performance.

本考案は、上述の実情に鑑みて、凝集処理のための構造
を利用した簡単な改良でもって、脱水機による脱水の処
理性能を向上できるようにして、含水率の低いろ過物並
びに浮遊物質濃度の低いろ過水を回収できるようにする
事を目的とする。
In view of the above-mentioned circumstances, the present invention has been developed to improve the dewatering performance of a dehydrator through a simple improvement using a structure for flocculation treatment, thereby reducing the concentration of filtrate with low water content and suspended solids. The purpose is to be able to recover filtered water with low filtration.

次に、本考案の実施例の態様を例示図に基いて詳述する
Next, aspects of embodiments of the present invention will be described in detail based on illustrative drawings.

水処理装置1で回収した処理汚泥をポンプ流路2を通し
て2基の凝集装置3,3に並列供給すると共に、その凝
集処理後の汚泥をベルトプレス型脱水機4に供給し、そ
のろ過物をホッパー5に、かつろ過水を流路6に回収す
るように汚泥処理設備を構成しである。
The treated sludge collected in the water treatment device 1 is supplied in parallel to two flocculation devices 3 through the pump channel 2, and the sludge after the flocculation treatment is supplied to the belt press type dehydrator 4, and the filtrate is The sludge treatment equipment is configured to collect the filtered water into the hopper 5 and the flow path 6.

前記凝集装置3を構成するに、ポリアクリルアミンやポ
リエチレンアミンに代表される高分子凝集剤などの有機
凝集剤、或は硫酸アルミニウムや硫酸第1鉄などの無機
凝集剤の供給管7と、前記ポンプ流路2からの水処理汚
泥の分岐供給管8を、混和槽9に接続すると共に、回転
駆動装置10とそれに攪拌翼体11を連設して成る攪拌
装置12を、その翼体11を凝集剤と水処理汚泥の供給
部近くに位置させて設けて、槽9内の汚泥含有水を槽内
で旋回流動させて供給される凝集剤と水処理汚泥を攪拌
混和させるようにし、そして槽内の汚泥含有水に対する
脱水の処理装置13を設けると共に、前記ベルトプレス
型脱水機4に対する凝集処理汚泥の供給管14を接続し
、かつ前記供給管7゜8.14の夫々に開閉弁15を設
けてあり、2基の凝集装置3,3における弁15の選択
的な開閉操作により、前記ベルトプレス型脱水機4に対
して凝集処理汚泥を交互に供給するようにしである。
The flocculation device 3 includes a supply pipe 7 for an organic flocculant such as a polymer flocculant typified by polyacrylamine or polyethylene amine, or an inorganic flocculant such as aluminum sulfate or ferrous sulfate; A branch supply pipe 8 for water treatment sludge from the pump flow path 2 is connected to a mixing tank 9, and a stirring device 12 consisting of a rotary drive device 10 and a stirring blade body 11 connected thereto is connected. The sludge-containing water in tank 9 is rotated and flowed in the tank, and the supplied flocculant and water treatment sludge are stirred and mixed. A dewatering device 13 is provided for the sludge-containing water in the tank, and a supply pipe 14 for coagulated sludge to the belt press type dehydrator 4 is connected, and an on-off valve 15 is provided in each of the supply pipes 7°, 8, and 14. The flocculated sludge is alternately supplied to the belt press type dehydrator 4 by selectively opening and closing the valves 15 in the two flocculating devices 3, 3.

前記脱水処理装置13を構成するに、第2図に示すよう
に、筒形状の枠組本体16の両側にそれと同芯状に筒支
軸17.17を一体連設すると共に、その枠組本体16
の周部にろ布18を張設して、ろ過部を有する中空回転
体19を形威し、この中空回転体19を、そのろ退部周
壁の一部を槽内の汚泥含有水の水面よりも上位に位置さ
せて、かつ前記汚泥含有水の旋回流動方向に交叉する水
平横軸芯周りで回転自在に槽壁にわたって架設すると共
に、それに対する回転駆動装置35を連設し、そして吸
引ポンプ20を備えた管路21とコンプレッサー22を
備えた管路23を、前記筒支軸17を通して中空回転体
19の内部に配設し、この内の吸引管路21を中空回転
体19の底部側に開口させて、前記周壁ろ退部を通して
浸透流入した中空回転体内の水を吸引排出させると共に
、他方の管路23にその長手方向に間隔をへだてて多数
のガス吹付はノズル24・・・・・・を設け、かつその
ノズル24・・・・・・を水面上方に位置するろ退部周
壁部分に沿わせね配設して、その噴出ガスによって前記
ろ退部に付着した汚泥を逆圧剥離させるようにし、そし
て逆圧剥離によって吹き飛ばされる汚泥の拡散を防止し
、かつそれを槽内に戻すカバー25を設けである。
As shown in FIG. 2, the dehydration treatment apparatus 13 is constructed by integrally connecting cylinder support shafts 17 and 17 on both sides of a cylindrical frame body 16 concentrically with the frame body 16.
A filter cloth 18 is stretched around the circumference of the hollow rotating body 19 to form a hollow rotating body 19 having a filtration part, and a part of the circumferential wall of the filtering part of the hollow rotating body 19 is connected to the water surface of the sludge-containing water in the tank. The suction pump is located above the sludge-containing water and is installed over the tank wall so as to be rotatable around the horizontal horizontal axis that intersects with the swirling flow direction of the sludge-containing water, and a rotation drive device 35 is connected thereto. A conduit 21 with a compressor 20 and a conduit 23 with a compressor 22 are disposed inside the hollow rotary body 19 through the cylinder support shaft 17, and the suction conduit 21 of these is connected to the bottom side of the hollow rotary body 19. The nozzles 24 are opened to suck and discharge the water in the hollow rotating body that has permeated through the peripheral wall filtration part, and the nozzles 24 are used to spray a large number of gases at intervals in the longitudinal direction of the other pipe 23. ... is provided, and its nozzle 24 is disposed not along the peripheral wall of the filtration section located above the water surface, and the sludge adhering to the filtration section is removed from the filtration section by back pressure. A cover 25 is provided to allow the sludge to be peeled off, to prevent the sludge blown away by the reverse pressure peeling from spreading, and to return it into the tank.

即ち、凝集装置3を構成する混和槽9を利用して、それ
に貯留の汚泥含有水中にろ退部を有する回転体19を設
けて、水処理汚泥に対する凝集の処理と同時にろ過水の
処理を行なわせると共に、ろ退部の付着汚泥を連続的に
ガス剥離させる事によって良好なろ過脱水を連続させ、
もって含水率を低くしてその脱水処理負荷を小にした凝
集処理汚泥をベルトプレス型脱水機4に供給するように
しである。
That is, the mixing tank 9 constituting the flocculation device 3 is used, and a rotary body 19 having a filtering section is provided in the sludge-containing water stored therein, and the filtrate is treated at the same time as the flocculation of the water treatment sludge. At the same time, the sludge adhering to the filtration section is continuously gas-separated to ensure good filtration and dewatering.
The flocculated sludge with a lower water content and a smaller dewatering load is supplied to the belt press type dehydrator 4.

前記ベルトプレス型脱水機4を構成するに、吸引ブロワ
を接続したダクト26の上面に多数の小孔を穿設し、こ
のダクト26の下部にジグザグ状に多数のローラー27
・・・・・・を架設すると共に、ダクト26の一端側に
駆動ローラー28を、かつダクト26の他端側と上部中
央部に緊張ローラー29.29を設け、更に、経路変曲
用と挟圧用およびろ過物剥離用と蛇行修正用のローラー
30・・・・・・を設け、そしてこれらのローラ一群に
わたって2枚の無端帯状ろ布31.31を巻き掛けると
共に、前記ダクト26の上部一端側に凝集処理汚泥の供
給部32を設けて、重力脱水ゾーンAとこれに続く螺圧
脱水ゾーンBおよび圧縮脱水ゾーンCと剪断脱水ゾーン
Dを構威し、もって凝集処理汚泥を順次脱水処理して、
そのろ過物をコンベア32から前記ホッパー5に、かつ
ろ過水を流路6に回収するようにしてあり、前記凝集装
置3から供給される凝集処理汚泥の含水率が低くて脱水
処理負荷が小であるから、回収ろ過物の含水率を低くシ
、処理量を多くする性能の良い脱水処理を行なわせられ
る。
To configure the belt press type dehydrator 4, a large number of small holes are bored in the upper surface of a duct 26 to which a suction blower is connected, and a large number of rollers 27 are arranged in a zigzag pattern in the lower part of this duct 26.
In addition, a drive roller 28 is provided at one end of the duct 26, and tension rollers 29 and 29 are provided at the other end and the center of the upper part of the duct 26. Rollers 30 for pressure, filter removal, and meandering correction are provided, and two endless belt-shaped filter cloths 31 and 31 are wrapped around a group of these rollers, and one end of the upper part of the duct 26 is provided. A supply unit 32 for flocculated sludge is provided in the sludge, and a gravity dewatering zone A is followed by a screw pressure dewatering zone B, a compression dewatering zone C, and a shear dewatering zone D, whereby the flocculated sludge is sequentially dehydrated. ,
The filtrate is collected from the conveyor 32 to the hopper 5, and the filtrate is collected to the flow path 6, and the water content of the flocculated sludge supplied from the flocculation device 3 is low, so that the dewatering load is small. Because of this, it is possible to perform highly efficient dehydration treatment that lowers the water content of the collected filtrate and increases the throughput.

第3図及び第4図は、夫々凝集装置3の変形構造を示し
、第3図に示すものは、前記ろ退部を有する中空回転体
19に対してそれの周部に翼体33を付設して、ろ布1
8に対して連続的に目詰りを解消するための回転体19
の回転構造を有効に利用して攪拌装置を構成してあり、
特別な攪拌装置12を省略すると共に、それによって装
置全体のコンパクト化を図る事ができる。
3 and 4 respectively show modified structures of the agglomerating device 3, and the one shown in FIG. 3 has a blade body 33 attached to the circumference of the hollow rotating body 19 having the filtering section. and filter cloth 1
Rotating body 19 for continuously eliminating clogging with respect to 8
The stirring device is constructed by effectively utilizing the rotating structure of
The special stirring device 12 can be omitted, and thereby the entire device can be made more compact.

第4図に示すものは、第1図に示す第1実施構造の凝集
装置3において、その混和槽9を壁体34で区画して攪
拌装置12を備える区画槽9aにおいて水処理汚泥と凝
集剤を攪拌混和すると共に、脱水処理装置13を備える
区画槽9bに対して凝集剤混和水を壁体34の上縁から
オーバーフローさせるようにしてあり、静水域の区画槽
9bにおいて汚泥含有水を脱水処理すると共に、その槽
9bの底部に凝集汚泥を沈澱させる事ができ、従って1
基の凝集装置3でもって、凝集汚泥を連続的に脱水機4
に供給する事も可能となる。
What is shown in FIG. 4 is the flocculation device 3 of the first implementation structure shown in FIG. At the same time, the flocculant-mixed water is caused to overflow from the upper edge of the wall body 34 to the divided tank 9b equipped with the dehydration treatment device 13, and the sludge-containing water is dehydrated in the still water compartment tank 9b. At the same time, the flocculated sludge can be settled at the bottom of the tank 9b, and therefore 1
The flocculated sludge is continuously transferred to the dehydrator 4 using the base flocculating device 3.
It is also possible to supply

尚、脱水機4として、遠心脱水型のものなど各種変更可
能である。
The dehydrator 4 can be modified in various ways, such as a centrifugal dehydrator.

以上要するに本考案は、雪起した凝集装置において、横
軸芯周りの周壁にろ退部を有する中空回転体を、その周
壁が混和槽内の汚泥含有水の水面に対して上下にわたる
状態で設け、前記中空回転体内の水を吸引排出する管路
を設け、前記ろ退部のうち前記混和槽内水面上方に位置
する部分に対してガスを吹付けるノズルを、前記中空回
転体の内部に設けである事を特徴とする。
In summary, the present invention provides a snow flocculation device in which a hollow rotary body having a filtering part on the peripheral wall around the horizontal axis is provided with the peripheral wall extending above and below the water surface of the sludge-containing water in the mixing tank. , a pipe line is provided for sucking and discharging the water in the hollow rotating body, and a nozzle is provided inside the hollow rotating body for blowing gas to a portion of the filtration section located above the water surface in the mixing tank. It is characterized by

即ち、凝集装置に対して極めて簡単な構造のろ過脱水の
装置を付加するだけの改良でもって、凝集の処理と同時
にそれの含水率を低くする前処理を行なわせられ、その
結果、脱水機による回収ろ過物の含水率を低下させ、処
理量を増大させる事ができその脱水性能を大幅に向上で
きる。
In other words, by simply adding a filtration and dehydration device with an extremely simple structure to the flocculation device, it is possible to carry out pretreatment to lower the water content at the same time as the flocculation process, and as a result, the dehydration device The water content of the collected filtrate can be lowered, the amount of treatment can be increased, and the dehydration performance can be greatly improved.

その上、ろ過脱水に伴って付着するろ退部の汚泥を順次
連続的にガス剥離させるので、汚泥濃度を低下させるよ
うな事なく、その性能の良いろ過脱水状態を良好に維持
させる事ができる。
Furthermore, since the sludge that adheres to the filtration section during filtration and dewatering is sequentially and continuously gas-stripped, the filtration and dehydration conditions with good performance can be maintained without reducing the sludge concentration. .

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案に係る脱水機用凝集装置の実施の態様を例
示し、第1図は汚泥処理設備の概略全体縦断面図、第2
図は第1図のII −II線断面図、第3図及び第4図
は、夫々凝集装置の変形構造を示す断面図である。 4・・・・・・脱水機、9・・・・・・混和槽、19・
・・・・・中空回転体、21・・・・・・吸引排出管路
、24・・・・・・ノズル。
The drawings illustrate an embodiment of the dehydrator agglomeration device according to the present invention, and FIG. 1 is a schematic longitudinal sectional view of the entire sludge treatment facility, and FIG.
The figure is a sectional view taken along the line II--II of FIG. 1, and FIGS. 3 and 4 are sectional views showing modified structures of the agglomerating device, respectively. 4... Dehydrator, 9... Mixing tank, 19.
...Hollow rotating body, 21 ... Suction and discharge pipe, 24 ... Nozzle.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 脱水機4へ供給前処理として水処理汚泥と凝集剤とを混
和するための凝集装置であって、横軸芯周りの周壁にろ
過部を有する中空回転体19を、その周壁が混和槽9内
の汚泥含有水の水面に対して上下にわたる状態で設け、
前記中空回転体19内の水を吸引排出する管路21を設
け、前記ろ過部のうち前記混和槽9内水面上方に位置す
る部分に対してガスを吹付けるノズル24・・・・・・
を、前記中空回転体19の内部に設けである事を特徴と
する脱水機用凝集装置。
This is a flocculating device for mixing water treatment sludge and a flocculant as a pre-treatment for supply to the dehydrator 4, and includes a hollow rotating body 19 having a filtration part on the peripheral wall around the horizontal axis, the peripheral wall of which is inside the mixing tank 9. installed above and below the water surface of the sludge-containing water,
A pipe line 21 for sucking and discharging the water in the hollow rotating body 19 is provided, and a nozzle 24 for spraying gas onto a portion of the filtration section located above the water surface in the mixing tank 9.
A coagulating device for a dehydrator, characterized in that the above-mentioned hollow rotating body 19 is provided with:
JP8900379U 1979-06-27 1979-06-27 Coagulation device for dehydrator Expired JPS586488Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8900379U JPS586488Y2 (en) 1979-06-27 1979-06-27 Coagulation device for dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8900379U JPS586488Y2 (en) 1979-06-27 1979-06-27 Coagulation device for dehydrator

Publications (2)

Publication Number Publication Date
JPS567514U JPS567514U (en) 1981-01-22
JPS586488Y2 true JPS586488Y2 (en) 1983-02-04

Family

ID=29322172

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8900379U Expired JPS586488Y2 (en) 1979-06-27 1979-06-27 Coagulation device for dehydrator

Country Status (1)

Country Link
JP (1) JPS586488Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59120096U (en) * 1983-02-02 1984-08-13 オルガノ株式会社 Sludge agitation supply device for filter cloth running type dehydrator

Also Published As

Publication number Publication date
JPS567514U (en) 1981-01-22

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